RU2010102493A - BIOFUEL COMPOSITION, METHOD FOR ITS MANUFACTURE AND METHOD FOR ITS FILLING - Google Patents

BIOFUEL COMPOSITION, METHOD FOR ITS MANUFACTURE AND METHOD FOR ITS FILLING Download PDF

Info

Publication number
RU2010102493A
RU2010102493A RU2010102493/05A RU2010102493A RU2010102493A RU 2010102493 A RU2010102493 A RU 2010102493A RU 2010102493/05 A RU2010102493/05 A RU 2010102493/05A RU 2010102493 A RU2010102493 A RU 2010102493A RU 2010102493 A RU2010102493 A RU 2010102493A
Authority
RU
Russia
Prior art keywords
vol
concentration
vegetable oils
fuel
composition according
Prior art date
Application number
RU2010102493/05A
Other languages
Russian (ru)
Inventor
Гопалкришна Мангалоре КИНИ (IN)
Гопалкришна Мангалоре КИНИ
Чандрасекар Бхаскаран НЭР (IN)
Чандрасекар Бхаскаран НЭР
Пханикумар ПУЛЛЕЛА (IN)
Пханикумар ПУЛЛЕЛА
Пиларисетти Венката СУББАРАО (IN)
Пиларисетти Венката СУББАРАО
Original Assignee
Бигтек Прайвит Лимитид (In)
Бигтек Прайвит Лимитид
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Бигтек Прайвит Лимитид (In), Бигтек Прайвит Лимитид filed Critical Бигтек Прайвит Лимитид (In)
Publication of RU2010102493A publication Critical patent/RU2010102493A/en

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/02Liquid carbonaceous fuels essentially based on components consisting of carbon, hydrogen, and oxygen only
    • C10L1/026Liquid carbonaceous fuels essentially based on components consisting of carbon, hydrogen, and oxygen only for compression ignition
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G2300/00Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
    • C10G2300/10Feedstock materials
    • C10G2300/1011Biomass
    • C10G2300/1014Biomass of vegetal origin
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G2300/00Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
    • C10G2300/10Feedstock materials
    • C10G2300/1037Hydrocarbon fractions
    • C10G2300/1048Middle distillates
    • C10G2300/1051Kerosene having a boiling range of about 180 - 230 °C
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G2300/00Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
    • C10G2300/10Feedstock materials
    • C10G2300/1037Hydrocarbon fractions
    • C10G2300/1048Middle distillates
    • C10G2300/1055Diesel having a boiling range of about 230 - 330 °C
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G2300/00Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
    • C10G2300/80Additives
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/10Biofuels, e.g. bio-diesel
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P30/00Technologies relating to oil refining and petrochemical industry
    • Y02P30/20Technologies relating to oil refining and petrochemical industry using bio-feedstock

Abstract

1. Биотопливная композиция, включающая дистиллированную техническую жидкость из скорлупы ореха кешью (ДТ-ЖСК) в концентрации от 0,1 до 30 об.% и, по меньшей мере, один нефтепродукт, выбранный из группы, включающей дизельное топливо и керосин, в концентрации от 70 до 99,9 об.%, необязательно в смеси с растительными маслами и по меньшей мере одной топливной присадкой. ! 2. Композиция по п.1, в которой ДТ-ЖСК включает карданол, кардол и метилкардол в следующих концентрациях, об.%: ! карданол 75÷99,8 кардол 0,01÷12,5 метилкардол 0,01÷12,5 ! 3. Композиция по п.1, в которой дизельное топливо и керосин содержатся в соотношении от 9,5÷0,5 об.% до 0,5÷9,5 об.%. ! 4. Композиция по п.1, в которой по меньшей мере одна топливная присадка выбрана из группы, включающей антиполимеризаторы, антидетонационные присадки, присадки-антифризы, антикоагулянты, антиосадители, присадки, повышающие цетановый индекс, и присадки, повышающие цетановое число, или любые их комбинации. ! 5. Композиция по п.4, в которой по меньшей мере одна топливная присадка содержится в концентрации от 0,01 до 5 об.%, предпочтительно от 0,01 до 1 об.%. ! 6. Композиция по п.4, в которой топливной присадкой является антиполимеризатор. ! 7. Композиция по п.4, в которой антиполимеризатор выбран из группы, включающей трифенилфосфит (ТФФ), тринонилфенилфосфит (ТНФФ), диизодецилфенилфосфит (ДДФФ), дифенилизооктилфосфит (ДФОФ), дифенилизодецилфосфит (ДФДФ), трикрезилфосфат (ТКФ), крезилдифенилфосфат (КДФ), динитрофенол, гидрохинон, пара-крезол, динитро-пара-крезол, метиловый эфир гидрохинона, полигидрохинон и поли-α-нафтол или любые их комбинации. ! 8. Композиция по п.1, в которой растительные масла выбраны из гру 1. Biofuel composition comprising distilled technical liquid from cashew nut shells (DT-ZhSK) at a concentration of 0.1 to 30 vol.% And at least one oil product selected from the group including diesel fuel and kerosene at a concentration from 70 to 99.9 vol.%, optionally in a mixture with vegetable oils and at least one fuel additive. ! 2. Composition according to claim 1, in which DT-ZhSK includes cardanol, cardol and methylcardol in the following concentrations, vol.%:! cardanol 75 ÷ 99.8 cardol 0.01 ÷ 12.5 methyl cardol 0.01 ÷ 12.5! 3. The composition according to claim 1, in which diesel fuel and kerosene are contained in a ratio of from 9.5 ÷ 0.5 vol.% To 0.5 ÷ 9.5 vol.%. ! 4. The composition of claim 1, wherein at least one fuel additive is selected from the group consisting of anti-polymerization agents, anti-knock additives, anti-freeze additives, anticoagulants, anti-precipitants, cetane index additives, and cetane number improvers, or any of them combinations. ! 5. A composition according to claim 4, wherein the at least one fuel additive is present in a concentration of 0.01 to 5 vol%, preferably 0.01 to 1 vol%. ! 6. The composition of claim 4, wherein the fuel additive is an antipolymerization agent. ! 7. A composition according to claim 4, in which the antipolymerizer is selected from the group consisting of triphenylphosphite (TPP), trinonylphenylphosphite (TNPP), diisodecylphenylphosphite (DPPP), diphenylisoctylphosphite (DPOF), diphenylisodecylphosphite (DPPD), kaphenylphosphite) , dinitrophenol, hydroquinone, para-cresol, dinitro-para-cresol, hydroquinone methyl ester, polyhydroquinone and poly-α-naphthol, or any combination thereof. ! 8. The composition according to claim 1, in which the vegetable oils are selected from

Claims (38)

1. Биотопливная композиция, включающая дистиллированную техническую жидкость из скорлупы ореха кешью (ДТ-ЖСК) в концентрации от 0,1 до 30 об.% и, по меньшей мере, один нефтепродукт, выбранный из группы, включающей дизельное топливо и керосин, в концентрации от 70 до 99,9 об.%, необязательно в смеси с растительными маслами и по меньшей мере одной топливной присадкой.1. Biofuel composition, including distilled technical liquid from cashew nutshell (DT-ZhSK) in a concentration of from 0.1 to 30 vol.% And at least one petroleum product selected from the group comprising diesel fuel and kerosene, in a concentration from 70 to 99.9 vol.%, optionally in a mixture with vegetable oils and at least one fuel additive. 2. Композиция по п.1, в которой ДТ-ЖСК включает карданол, кардол и метилкардол в следующих концентрациях, об.%:2. The composition according to claim 1, in which DT-HSC includes cardanol, cardol and methyl cardol in the following concentrations, vol.%: карданолcardanol 75÷99,875 ÷ 99.8 кардолcardol 0,01÷12,50.01 ÷ 12.5 метилкардолmethylcardol 0,01÷12,50.01 ÷ 12.5
3. Композиция по п.1, в которой дизельное топливо и керосин содержатся в соотношении от 9,5÷0,5 об.% до 0,5÷9,5 об.%.3. The composition according to claim 1, in which diesel fuel and kerosene are contained in a ratio of from 9.5 ÷ 0.5 vol.% To 0.5 ÷ 9.5 vol.%. 4. Композиция по п.1, в которой по меньшей мере одна топливная присадка выбрана из группы, включающей антиполимеризаторы, антидетонационные присадки, присадки-антифризы, антикоагулянты, антиосадители, присадки, повышающие цетановый индекс, и присадки, повышающие цетановое число, или любые их комбинации.4. The composition according to claim 1, in which at least one fuel additive is selected from the group comprising antipolymerization agents, antiknock additives, antifreeze additives, anticoagulants, antioxidants, additives that increase the cetane index, and additives that increase the cetane number, or any of them combinations. 5. Композиция по п.4, в которой по меньшей мере одна топливная присадка содержится в концентрации от 0,01 до 5 об.%, предпочтительно от 0,01 до 1 об.%.5. The composition according to claim 4, in which at least one fuel additive is contained in a concentration of from 0.01 to 5 vol.%, Preferably from 0.01 to 1 vol.%. 6. Композиция по п.4, в которой топливной присадкой является антиполимеризатор.6. The composition according to claim 4, in which the fuel additive is an antipolymerization agent. 7. Композиция по п.4, в которой антиполимеризатор выбран из группы, включающей трифенилфосфит (ТФФ), тринонилфенилфосфит (ТНФФ), диизодецилфенилфосфит (ДДФФ), дифенилизооктилфосфит (ДФОФ), дифенилизодецилфосфит (ДФДФ), трикрезилфосфат (ТКФ), крезилдифенилфосфат (КДФ), динитрофенол, гидрохинон, пара-крезол, динитро-пара-крезол, метиловый эфир гидрохинона, полигидрохинон и поли-α-нафтол или любые их комбинации.7. The composition according to claim 4, in which the antipolymerization agent is selected from the group consisting of triphenylphosphite (TFF), trinonylphenylphosphite (THFF), diisodecylphenylphosphite (DDPF), diphenylisooctylphosphite (DFOF), diphenylisodecylphosphite (KDF) CDF , dinitrophenol, hydroquinone, para-cresol, dinitro-para-cresol, hydroquinone methyl ester, polyhydroquinone and poly-α-naphthol, or any combination thereof. 8. Композиция по п.1, в которой растительные масла выбраны из группы, включающей рапсовое масло, пальмовое масло, касторовое масло, подсолнечное масло, сафлоровое масло, конопляное масло, горчичное масло, соевое масло, масло барбадосского ореха, масло из семян редиса, масло канолы, кукурузное масло, масло из отрубей риса, арахисовое масло, хлопковое масло, кокосовое масло, масло из косточек дерева ним и тунговое масло или любые их комбинации.8. The composition according to claim 1, in which the vegetable oils are selected from the group comprising rapeseed oil, palm oil, castor oil, sunflower oil, safflower oil, hemp oil, mustard oil, soybean oil, Barbados nut oil, radish seed oil, canola oil, corn oil, rice bran oil, peanut oil, cottonseed oil, coconut oil, neem tree oil and tung oil, or any combination thereof. 9. Композиция по п.8, в которой растительные масла присутствуют в концентрации от 4 до 29 об.%.9. The composition of claim 8, in which vegetable oils are present in a concentration of from 4 to 29 vol.%. 10. Композиция по п.8, в которой растительные масла используют в виде их метиловых эфиров.10. The composition of claim 8, in which vegetable oils are used in the form of their methyl esters. 11. Композиция по п.1, включающая ДТ-ЖСК в концентрации приблизительно 4,5 об.% и дизельное топливо в концентрации приблизительно 95,5 об.% необязательно в смеси с растительными маслами и по меньшей мере одной топливной присадкой.11. The composition according to claim 1, comprising DT-HBC at a concentration of approximately 4.5 vol.% And diesel fuel at a concentration of approximately 95.5 vol.% Optionally mixed with vegetable oils and at least one fuel additive. 12. Композиция по п.1, включающая ДТ-ЖСК в концентрации приблизительно 5 об.% и дизельное топливо в концентрации приблизительно 95 об.% необязательно в смеси с растительными маслами и по меньшей мере одной топливной присадкой.12. The composition according to claim 1, comprising DT-HBC at a concentration of about 5 vol.% And diesel fuel at a concentration of about 95 vol.% Optionally mixed with vegetable oils and at least one fuel additive. 13. Композиция по п.1, включающая ДТ-ЖСК в концентрации приблизительно 10 об.% и дизельное топливо в концентрации приблизительно 90 об.%, необязательно в смеси с растительными маслами и по меньшей мере одной топливной присадкой.13. The composition according to claim 1, comprising DT-HBC at a concentration of about 10 vol.% And diesel fuel at a concentration of about 90 vol.%, Optionally mixed with vegetable oils and at least one fuel additive. 14. Композиция по п.1, включающая ДТ-ЖСК в концентрации приблизительно 15 об.% и дизельное топливо в концентрации приблизительно 85 об.% необязательно в смеси с растительными маслами и по меньшей мере одной топливной присадкой.14. The composition according to claim 1, comprising DT-HBC at a concentration of about 15 vol.% And diesel fuel at a concentration of about 85 vol.% Optionally mixed with vegetable oils and at least one fuel additive. 15. Композиция по п.1, включающая ДТ-ЖСК в концентрации приблизительно 20 об.% и дизельное топливо в концентрации приблизительно 80 об.% необязательно в смеси с растительными маслами и по меньшей мере одной топливной присадкой.15. The composition according to claim 1, comprising DT-HBC at a concentration of about 20 vol.% And diesel fuel at a concentration of about 80 vol.% Optionally mixed with vegetable oils and at least one fuel additive. 16. Композиция по п.1, включающая ДТ-ЖСК в концентрации приблизительно 5 об.% и керосин в концентрации приблизительно 95 об.% необязательно в смеси с растительными маслами и по меньшей мере одной топливной присадкой.16. The composition according to claim 1, comprising DT-HSC at a concentration of about 5 vol.% And kerosene at a concentration of about 95 vol.% Optionally mixed with vegetable oils and at least one fuel additive. 17. Композиция по п.1, включающая ДТ-ЖСК в концентрации приблизительно 10 об.% и керосин в концентрации приблизительно 90 об.% необязательно в смеси с растительными маслами и по меньшей мере одной топливной присадкой.17. The composition according to claim 1, comprising DT-HSC at a concentration of about 10 vol.% And kerosene at a concentration of about 90 vol.% Optionally mixed with vegetable oils and at least one fuel additive. 18. Композиция по п.1, включающая ДТ-ЖСК в концентрации приблизительно 15 об.% и керосин в концентрации приблизительно 85 об.% необязательно в смеси с растительными маслами и по меньшей мере одной топливной присадкой.18. The composition according to claim 1, comprising DT-HSC at a concentration of about 15 vol.% And kerosene at a concentration of about 85 vol.% Optionally mixed with vegetable oils and at least one fuel additive. 19. Композиция по п.1, включающая ДТ-ЖСК в концентрации 5 об.%, дизельное топливо в концентрации 90 об.% и керосин в концентрации 5 об.% необязательно в смеси с растительными маслами и по меньшей мере одной топливной присадкой.19. The composition according to claim 1, comprising DT-HBC at a concentration of 5 vol.%, Diesel fuel at a concentration of 90 vol.% And kerosene at a concentration of 5 vol.% Optionally mixed with vegetable oils and at least one fuel additive. 20. Композиция по п.1, включающая ДТ-ЖСК в концентрации приблизительно 5 об.%, дизельное топливо в концентрации приблизительно 5 об.% и керосин в концентрации приблизительно 90 об.% необязательно в смеси с растительными маслами и по меньшей мере одной топливной присадкой.20. The composition according to claim 1, comprising DT-HBC at a concentration of about 5 vol.%, Diesel fuel at a concentration of about 5 vol.% And kerosene at a concentration of about 90 vol.% Optionally mixed with vegetable oils and at least one fuel oil additive. 21. Композиция по п.1, включающая ДТ-ЖСК в концентрации приблизительно 10 об.%, дизельное топливо в концентрации приблизительно 5 об.% и керосин в концентрации приблизительно 85 об.% необязательно в смеси с растительными маслами и по меньшей мере одной топливной присадкой.21. The composition according to claim 1, comprising DT-HBC at a concentration of about 10 vol.%, Diesel fuel at a concentration of about 5 vol.% And kerosene at a concentration of about 85 vol.% Optionally mixed with vegetable oils and at least one fuel oil additive. 22. Композиция по п.1, в которой ДТ-ЖСК включает полимерный материал в концентрации менее 5 об.%.22. The composition according to claim 1, in which DT-HSC includes a polymer material in a concentration of less than 5 vol.%. 23. Способ изготовления биотопливной композиции, которая включает ДТ-ЖСК в концентрации от 0,1 до 30 об.% и, по меньшей мере, один нефтепродукт, выбранный из группы, включающей дизельное топливо и керосин, в концентрации от 70 до 99,9 об.% необязательно в смеси с растительными маслами и по меньшей мере одной топливной присадкой, характеризующийся смешиванием указанной ДТ-ЖСК, по меньшей мере, с одним нефтепродуктом, выбранным из группы, включающей дизельное топливо и керосин, необязательно в смеси с растительными маслами и по меньшей мере одной топливной присадкой.23. A method of manufacturing a biofuel composition, which includes DT-HSC in a concentration of from 0.1 to 30 vol.% And at least one petroleum product selected from the group comprising diesel fuel and kerosene, in a concentration of from 70 to 99.9 vol.% optionally mixed with vegetable oils and at least one fuel additive, characterized by mixing said DT-HSC with at least one petroleum product selected from the group consisting of diesel fuel and kerosene, optionally mixed with vegetable oils and at least one fuel willow additive. 24. Способ по п.23, в котором ДТ-ЖСК получают путем дистилляции технической ЖСК (жидкости из скорлупы ореха кешью).24. The method according to item 23, in which the DT-HSC is obtained by distillation of technical HBC (liquid cashew nutshell). 25. Способ по п.24, в котором дистилляцию технической ЖСК проводят при пониженном давлении в диапазоне от 1 до 15 мм рт.ст. и температуре в диапазоне от 225 до 275°С или при атмосферном давлении и температуре приблизительно 360°С.25. The method according to paragraph 24, in which the distillation of the technical HBC is carried out under reduced pressure in the range from 1 to 15 mm RT.article. and a temperature in the range of 225 to 275 ° C. or at atmospheric pressure and a temperature of approximately 360 ° C. 26. Способ по п.23, в котором биотопливную композицию дополнительно хранят в сухом помещении при температуре от -10 до 55°С.26. The method according to item 23, in which the biofuel composition is additionally stored in a dry room at a temperature of from -10 to 55 ° C. 27. Способ по п.23, в котором биотопливная композиция включает ДТ-ЖСК в концентрации от 4,5 до 20 об.% и дизельное топливо в концентрации от 80 до 95,5 об.% необязательно в смеси с растительными маслами и по меньшей мере одной топливной присадкой.27. The method according to item 23, in which the biofuel composition includes DT-HSC in a concentration of from 4.5 to 20 vol.% And diesel fuel in a concentration of from 80 to 95.5 vol.% Optionally in a mixture with vegetable oils and at least at least one fuel additive. 28. Способ по п.23, в котором биотопливная композиция включает ДТ-ЖСК в концентрации приблизительно 4,5 об.% и дизельное топливо в концентрации приблизительно 95,5 об.% необязательно в смеси с растительными маслами и по меньшей мере одной топливной присадкой.28. The method according to item 23, in which the biofuel composition includes DT-HBC at a concentration of approximately 4.5 vol.% And diesel fuel at a concentration of approximately 95.5 vol.% Optionally mixed with vegetable oils and at least one fuel additive . 29. Способ по п.23, в котором биотопливная композиция включает ДТ-ЖСК в концентрации приблизительно 10 об.% и дизельное топливо в концентрации приблизительно 90 об.% необязательно в смеси с растительными маслами и по меньшей мере одной топливной присадкой.29. The method according to item 23, in which the biofuel composition includes DT-HBC at a concentration of about 10 vol.% And diesel fuel at a concentration of about 90 vol.% Optionally mixed with vegetable oils and at least one fuel additive. 30. Способ по п.23, в котором биотопливная композиция включает ДТ-ЖСК в концентрации от 5 до 15 об.% и керосин в концентрации от 85 до 95 об.% необязательно в смеси с растительными маслами и по меньшей мере одной топливной присадкой.30. The method according to item 23, in which the biofuel composition includes DT-HSC in a concentration of from 5 to 15 vol.% And kerosene in a concentration of from 85 to 95 vol.% Optionally mixed with vegetable oils and at least one fuel additive. 31. Способ по п.23, в котором биотопливная композиция включает ДТ-ЖСК в концентрации от 5 до 10 об.%, дизельное топливо в концентрации от 5 до 95 об.% и керосин в концентрации от 5 до 90 об.% необязательно в смеси с растительными маслами и по меньшей мере одной топливной присадкой.31. The method according to item 23, in which the biofuel composition includes DT-HSC in a concentration of from 5 to 10 vol.%, Diesel fuel in a concentration of from 5 to 95 vol.% And kerosene in a concentration of from 5 to 90 vol.% mixtures with vegetable oils and at least one fuel additive. 32. Способ заправки биотопливной композицией, включающей ДТ-ЖСК в концентрации от 0,1 до 30 об.% и, по меньшей мере, один нефтепродукт, выбранный из группы, включающей дизельное топливо и керосин, в концентрации от 70 до 99,9 об.% необязательно в смеси с растительными маслами и по меньшей мере одной топливной присадкой, характеризующийся заправкой биотопливной композицией в различные топливные агрегаты.32. A method of refueling with a biofuel composition comprising DT-ZhSK in a concentration of from 0.1 to 30 vol.% And at least one petroleum product selected from the group comprising diesel fuel and kerosene in a concentration of from 70 to 99.9 vol. .% optionally mixed with vegetable oils and at least one fuel additive, characterized by filling the biofuel composition into various fuel assemblies. 33. Способ по п.32, в котором топливные агрегаты выбраны из группы, включающей агрегаты для отопления помещений, освещения, для приготовления пищи, двигатели автомобилей, насосов и генераторов.33. The method according to p, in which the fuel units are selected from the group including units for heating rooms, lighting, for cooking, car engines, pumps and generators. 34. Способ по п.32, в котором биотопливная композиция включает ДТ-ЖСК в концентрации от 4,5 до 20 об.% и дизельное топливо в концентрации от 80 до 95,5 об.% необязательно в смеси с растительными маслами и по меньшей мере одной топливной присадкой.34. The method according to p, in which the biofuel composition includes DT-HSC in a concentration of from 4.5 to 20 vol.% And diesel fuel in a concentration of from 80 to 95.5 vol.% Optionally in a mixture with vegetable oils and at least at least one fuel additive. 35. Способ по п.32, в котором биотопливная композиция включает ДТ-ЖСК в концентрации приблизительно 4,5 об.% и дизельное топливо в концентрации приблизительно 95,5 об.% необязательно в смеси с растительными маслами и по меньшей мере одной топливной присадкой.35. The method according to p, in which the biofuel composition includes DT-HBC at a concentration of approximately 4.5 vol.% And diesel fuel at a concentration of approximately 95.5 vol.% Optionally mixed with vegetable oils and at least one fuel additive . 36. Способ по п.32, в котором биотопливная композиция включает ДТ-ЖСК в концентрации приблизительно 10 об.% и дизельное топливо в концентрации приблизительно 90 об.% необязательно в смеси с растительными маслами и по меньшей мере одной топливной присадкой.36. The method according to p, in which the biofuel composition includes DT-HBC at a concentration of about 10 vol.% And diesel fuel at a concentration of about 90 vol.% Optionally mixed with vegetable oils and at least one fuel additive. 37. Способ по п.32, в котором биотопливная композиция включает ДТ-ЖСК в концентрации от 5 до 15 об.% и керосин в концентрации от 85 до 95 об.% необязательно в смеси с растительными маслами и по меньшей мере одной топливной присадкой.37. The method according to p, in which the biofuel composition includes DT-HSC in a concentration of from 5 to 15 vol.% And kerosene in a concentration of from 85 to 95 vol.% Optionally mixed with vegetable oils and at least one fuel additive. 38. Способ по п.32, в котором биотопливная композиция включает ДТ-ЖСК в концентрации от 5 до 10 об.%, дизельное топливо в концентрации от 5 до 95 об.% и керосин в концентрации от 5 до 90 об.% необязательно в смеси с растительными маслами и по меньшей мере одной топливной присадкой. 38. The method according to p, in which the biofuel composition includes DT-HSC in a concentration of from 5 to 10 vol.%, Diesel fuel in a concentration of from 5 to 95 vol.% And kerosene in a concentration of from 5 to 90 vol.% mixtures with vegetable oils and at least one fuel additive.
RU2010102493/05A 2007-06-29 2008-06-26 BIOFUEL COMPOSITION, METHOD FOR ITS MANUFACTURE AND METHOD FOR ITS FILLING RU2010102493A (en)

Applications Claiming Priority (4)

Application Number Priority Date Filing Date Title
IN1396CH2007 2007-06-29
IN01396/CHE/2007 2007-06-29
IN02925/CHE/2007 2007-12-06
IN2925CH2007 2007-12-06

Publications (1)

Publication Number Publication Date
RU2010102493A true RU2010102493A (en) 2011-08-10

Family

ID=40225735

Family Applications (1)

Application Number Title Priority Date Filing Date
RU2010102493/05A RU2010102493A (en) 2007-06-29 2008-06-26 BIOFUEL COMPOSITION, METHOD FOR ITS MANUFACTURE AND METHOD FOR ITS FILLING

Country Status (12)

Country Link
US (1) US8282692B2 (en)
EP (1) EP2164931A4 (en)
JP (1) JP5171946B2 (en)
KR (1) KR101194982B1 (en)
CN (1) CN101821366B (en)
AP (1) AP3033A (en)
AR (1) AR069363A1 (en)
BR (1) BRPI0813188A2 (en)
CA (1) CA2692459C (en)
MY (1) MY149322A (en)
RU (1) RU2010102493A (en)
WO (1) WO2009004652A1 (en)

Families Citing this family (46)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8308911B2 (en) 2009-01-09 2012-11-13 Cool Planet Biofuels, Llc System and method for atmospheric carbon sequestration
US9909067B2 (en) 2009-01-21 2018-03-06 Cool Planet Energy Systems, Inc. Staged biomass fractionator
CN102292414A (en) 2009-01-21 2011-12-21 酷星生物燃料有限公司 System and method for biomass fractioning
US8137628B2 (en) 2011-03-24 2012-03-20 Cool Planet Biofuels, Inc. System for making renewable fuels
US8143464B2 (en) 2011-03-24 2012-03-27 Cool Planet Biofuels, Inc. Method for making renewable fuels
US8431757B2 (en) 2011-03-24 2013-04-30 Cool Planet Biofuels, Inc. Method for making renewable fuels
US8951476B2 (en) 2011-03-24 2015-02-10 Cool Planet Energy Systems, Inc. System for making renewable fuels
US8173044B1 (en) 2011-05-09 2012-05-08 Cool Planet Biofuels, Inc. Process for biomass conversion to synthesis gas
US8367881B2 (en) 2011-05-09 2013-02-05 Cool Planet Biofuels, Inc. Method for biomass fractioning by enhancing biomass thermal conductivity
US8568493B2 (en) 2011-07-25 2013-10-29 Cool Planet Energy Systems, Inc. Method for producing negative carbon fuel
US8317891B1 (en) 2011-06-06 2012-11-27 Cool Planet Biofuels, Inc. Method for enhancing soil growth using bio-char
US10640429B2 (en) 2011-06-06 2020-05-05 Cool Planet Energy System, Inc. Methods for application of biochar
US10252951B2 (en) 2011-06-06 2019-04-09 Cool Planet Energy Systems, Inc. Biochars and biochar treatment processes
US10233129B2 (en) 2011-06-06 2019-03-19 Cool Planet Energy Systems, Inc. Methods for application of biochar
US11214528B2 (en) 2011-06-06 2022-01-04 Carbon Technology Holdings, LLC Treated biochar for use in water treatment systems
US9493380B2 (en) 2011-06-06 2016-11-15 Cool Planet Energy Systems, Inc. Method for enhancing soil growth using bio-char
US10173937B2 (en) 2011-06-06 2019-01-08 Cool Planet Energy Systems, Inc. Biochar as a microbial carrier
US9216916B2 (en) 2013-10-25 2015-12-22 Cool Planet Energy Systems, Inc. System and method for purifying process water produced from biomass conversion to fuels
US10118870B2 (en) 2011-06-06 2018-11-06 Cool Planet Energy Systems, Inc. Additive infused biochar
US9980912B2 (en) 2014-10-01 2018-05-29 Cool Planet Energy Systems, Inc. Biochars for use with animals
US11279662B2 (en) 2011-06-06 2022-03-22 Carbon Technology Holdings, LLC Method for application of biochar in turf grass and landscaping environments
US9809502B2 (en) 2011-06-06 2017-11-07 Cool Planet Energy Systems, Inc. Enhanced Biochar
US10696603B2 (en) 2011-06-06 2020-06-30 Carbon Technology Holdings, LLC Mineral solubilizing microorganism infused biochars
US10059634B2 (en) 2011-06-06 2018-08-28 Cool Planet Energy Systems, Inc. Biochar suspended solution
US10392313B2 (en) 2011-06-06 2019-08-27 Cool Planet Energy Systems, Inc. Method for application of biochar in turf grass and landscaping environments
US10322389B2 (en) 2014-10-01 2019-06-18 Cool Planet Energy Systems, Inc. Biochar aggregate particles
US10550044B2 (en) 2011-06-06 2020-02-04 Cool Planet Energy Systems, Inc. Biochar coated seeds
US9493379B2 (en) 2011-07-25 2016-11-15 Cool Planet Energy Systems, Inc. Method for the bioactivation of biochar for use as a soil amendment
US20130015099A1 (en) 2011-07-14 2013-01-17 Cool Planet Biofuels, Inc. Liquid fuel composition
US9260666B2 (en) 2011-07-25 2016-02-16 Cool Planet Energy Systems, Inc. Method for reducing the carbon footprint of a conversion process
EP2584025A1 (en) * 2011-10-21 2013-04-24 Infineum International Limited Lubricating oil composition
JP5990404B2 (en) * 2012-05-31 2016-09-14 出光興産株式会社 FUEL OIL BASE, METHOD FOR PRODUCING THE FUEL OIL BASE, AND FUEL OIL COMPOSITION CONTAINING THE FUEL OIL BASE
CN103509611B (en) * 2012-06-14 2015-08-05 刘粤荣 A kind of biofuel and preparation method thereof
ITVR20130251A1 (en) * 2013-11-22 2015-05-23 Bio S R L Fa METHOD FOR THE PRODUCTION OF A VEGETABLE FUEL STARTING FROM AN OIL OF ANACARDIO SHELLS
US11426350B1 (en) 2014-10-01 2022-08-30 Carbon Technology Holdings, LLC Reducing the environmental impact of farming using biochar
US10472297B2 (en) 2014-10-01 2019-11-12 Cool Planet Energy System, Inc. Biochars for use in composting
US10870608B1 (en) 2014-10-01 2020-12-22 Carbon Technology Holdings, LLC Biochar encased in a biodegradable material
WO2016054431A1 (en) 2014-10-01 2016-04-07 Cool Planet Energy Systems, Inc. Biochars and biochar treatment processes
US11097241B2 (en) 2014-10-01 2021-08-24 Talipot Cool Extract (Ip), Llc Biochars, biochar extracts and biochar extracts having soluble signaling compounds and method for capturing material extracted from biochar
US11053171B2 (en) 2014-10-01 2021-07-06 Carbon Technology Holdings, LLC Biochars for use with animals
KR101728837B1 (en) 2014-11-28 2017-04-20 연세대학교 원주산학협력단 Method for decreasing ash and increasing oxidative stability in Cashew nuts shell liquid
CN109154258A (en) 2016-05-19 2019-01-04 日本普瑞姆股份有限公司 Utilize the diesel generating system of bio-fuel
CR20170211A (en) * 2017-05-24 2017-08-11 3-102-735850 Soc De Responsabilidad Ltda ORGANIC PROCEDURE FOR THE POTENTIALIZATION OF CONVENTIONAL AVGAS AND BIOAVGAS WITH EMISSION REDUCTION
CR20170215A (en) * 2017-05-24 2017-08-11 3-102-733702 Soc De Responsabilidad Ltda ORGANIC MIXING PROCESS FOR THE POTENTIALIZATION OF FOSSIL GASOLINE AND BIOETHANOL WITH EMISSION REDUCTION.
CR20170213A (en) * 2017-05-24 2017-08-11 3-102-735873 Soc De Responsabilidad Ltda ORGANIC PROCESS FOR THE PREVENTION OF CORROSION AND EXTREME TEMPERATURES IN INTERNAL COMBUSTION ENGINES AND INDUSTRIAL PROCESSES COOLED BY LIQUIDS.
CA3086845A1 (en) 2017-12-15 2019-06-20 Cool Planet Energy Systems, Inc. Biochars and biochar extracts having soluble signaling compounds and method for capturing material extracted from biochar

Family Cites Families (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2559594A (en) * 1951-07-10 Distillation of acid-treated cashew
US2230995A (en) * 1937-12-10 1941-02-11 F S Kerr & Company Larvicide and insecticide and method of production thereof
GB587273A (en) * 1942-10-17 1947-04-21 Standard Oil Dev Co Improvements in or relating to diesel fuel compositions
US6797021B2 (en) * 2000-10-05 2004-09-28 Indian Oil Corporation Limited Process of preparation of novel mannich bases from hydrogenated and distilled cashew nut shell liquid (CNSL) for use as additive in liquid hydrocarbon fuels
WO2004003114A1 (en) * 2002-06-26 2004-01-08 Indian Oil Corporation Limited A fuel additive composition for stabilising blends of ethanol and a hydrocarbon
JP4987273B2 (en) * 2005-09-16 2012-07-25 富士フイルム株式会社 Diesel fuel containing fatty acid ester and method for producing the same
US8067653B2 (en) * 2006-07-14 2011-11-29 The Governors Of The University Of Alberta Methods for producing fuels and solvents
US7960322B2 (en) * 2007-10-26 2011-06-14 Chevron Oronite Company Llc Lubricating oil compositions comprising a biodiesel fuel and an antioxidant

Also Published As

Publication number Publication date
EP2164931A1 (en) 2010-03-24
MY149322A (en) 2013-08-30
US20100107475A1 (en) 2010-05-06
JP2010531912A (en) 2010-09-30
CN101821366A (en) 2010-09-01
JP5171946B2 (en) 2013-03-27
CN101821366B (en) 2014-08-13
CA2692459A1 (en) 2009-01-08
AP2010005127A0 (en) 2010-02-28
WO2009004652A1 (en) 2009-01-08
AP3033A (en) 2014-11-30
KR101194982B1 (en) 2012-10-26
EP2164931A4 (en) 2011-09-07
KR20100049045A (en) 2010-05-11
US8282692B2 (en) 2012-10-09
AR069363A1 (en) 2010-01-20
CA2692459C (en) 2013-01-22
BRPI0813188A2 (en) 2020-08-18

Similar Documents

Publication Publication Date Title
RU2010102493A (en) BIOFUEL COMPOSITION, METHOD FOR ITS MANUFACTURE AND METHOD FOR ITS FILLING
Chauhan et al. Practice of diesel fuel blends using alternative fuels: A review
Eryilmaz et al. Biodiesel production potential from oil seeds in Turkey
Mofijur et al. Effect of biodiesel from various feedstocks on combustion characteristics, engine durability and materials compatibility: A review
Murugesan et al. Bio-diesel as an alternative fuel for diesel engines—a review
Rashid et al. Biodiesel from Milo (Thespesia populnea L.) seed oil
Baldev et al. Unveiling algal cultivation using raceway ponds for biodiesel production and its quality assessment
Bello et al. The effects of transesterification on selected fuel properties of three vegetable oils
CN101914394A (en) High-performance clean methanol gasoline
Verma et al. Operational and environmental impact of biodiesel on engine performance
Knothe et al. Methyl esters (biodiesel) from and fatty acid profile of Gliricidia sepium seed oil
Kumar et al. Experimental investigation of performance and emission characteristics of DI CI engine with dual biodiesel blends of Mexicana Argemone and Mahua
US8557001B2 (en) Fuel formulations
Tyagi et al. Experimental investigation of neem methyl esters as biodiesel on CI engine
Krishnakumar et al. Physico-chemical properties of the biodiesel extracted from rubber seed oil using solid metal oxide catalysts
Patel et al. Performance analyis of CI engine using diesel and waste cooking oil blend
Bello et al. Fatty acid compositions of six Nigeria's vegetable oils and their methyl esters
Rajagopal et al. Cloud point of biodiesel and blends
Batista et al. Production and physicochemical characterization of methylic and ethylic biodiesel from canola oil/obtenção e caracterização do biodiesel de canola pelas rotas metílica e etílica
TÜCCAR et al. Experimental investigation of engine performance and emission characteristics of a diesel engine using blends containing microalgae biodiesel, n-butanol and diesel fuel
CN103642549A (en) Clean biodiesel and preparation method thereof
Aliyu et al. Binary blends of petrodiesel with biodiesels derived from soyabean and groundnut oils
Kadu et al. Use of vegetable oils by Transesterification method as CI Engines Fuels: A Technical Review
CA2557251A1 (en) Fuel compositions
Jiang et al. Exhaust emissions and combustion performances of ethylene glycol monomethyl ether palm oil monoester as a novel biodiesel

Legal Events

Date Code Title Description
FA94 Acknowledgement of application withdrawn (non-payment of fees)

Effective date: 20120607